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1.
激光片光源技术在水垫塘流场显示中的应用   总被引:3,自引:0,他引:3  
戴光清  吴燕华 《实验力学》1997,12(4):544-548
文中研制了一套以激光作片光源的流场显示装置,并对单股和双股射流水垫塘流场进行了可视化研究.流场显示表明:双股射流的水垫塘流动结构可划分为六个区域,比通常的单股射流塘内水流结构增加了股间混掺区和“动水垫”影响区两个流区.分析讨论指出,双股射流入塘后水舌扩散加快和产生动水垫效应是其流态优于单股射流的两个显著特征.本文成果将为以降低塘底动水压强和充分发挥水垫塘消能效率为目标的水垫塘优化设计与计算提供指导和依据  相似文献   

2.
水垫塘三元流态及消能特征的数值和实验研究   总被引:11,自引:0,他引:11  
采用数值模拟和实验测试相结合的方法对水利工程中高拱坝泄洪水垫塘三元流场进行研究.获得了详细的流态特征,得到了水垫塘三元典型流态概化图.研究了水垫塘消能特性,并据此将塘内水体划分为剪切消能区、撞击消能区和混掺消能区.计算和实验所得的速度场及底板最大冲击动压相比较,二者基本一致.  相似文献   

3.
台阶式溢洪道掺气特性的试验研究   总被引:3,自引:0,他引:3  
通过试验研究了台阶式溢洪道上的掺气现象以及掺气区域的划分,试验表明,台阶式溢洪道沿程掺气可以分为非掺气区、掺气发展区和掺气充分发展区等三个区域;断面掺气分为台阶影响的含气区、楔形清水区、水中气泡区和空中水滴区。试验还测量了台阶式溢洪道上的断面掺气浓度及其沿程分布,计算了断面含水率,提出了初始掺气点的计算方法。与光滑溢洪道相比较,台阶式溢洪道具有初始掺气点前移,掺气发生早,发展快,掺气浓度大等特点。  相似文献   

4.
"5 12"汶川地震震后龙门山山前地表塌陷成因探讨   总被引:1,自引:0,他引:1  
应用NND有限差分格式求解轴对称可压缩N-S方程,研究了不同驻室与 环境压力比条件下欠膨胀超声速射流近场的失稳特性. 计算结果表明欠膨胀超声速射流的失 稳机制根据射流激波结构的特征可分为3种失稳模式:具有规则反射激波结构和单一剪切层 特征的射流不稳定性;带有马赫反射激波结构和双剪切层特征的射流不稳定性;具有弯曲马 赫杆和高度欠膨胀射流的不稳定性. 对于欠膨胀超声速射流,沿射流方向重复出现拟周期性 的射流激波结构是射流稳定发展的特征,这种射流激波结构的消失是射流开始失稳的标志.  相似文献   

5.
欠膨胀超声速射流不稳定性机理的数值研究   总被引:2,自引:0,他引:2  
应用NND有限差分格式求解轴对称可压缩N-S方程,研究了不同驻室与环境压力比条件下欠膨胀超声速射流近场的失稳特性.计算结果表明欠膨胀超声速射流的失稳机制根据射流激波结构的特征可分为3种失稳模式:具有规则反射激波结构和单一剪切层特征的射流不稳定性;带有马赫反射激波结构和双剪切层特征的射流不稳定性;具有弯曲马赫杆和高度欠膨胀射流的不稳定性.对于欠膨胀超声速射流,沿射流方向重复出现拟周期性的射流激波结构是射流稳定发展的特征,这种射流激波结构的消失是射流开始失稳的标志.  相似文献   

6.
为了能够更好地了解不定源喷嘴(indeterminate origin nozzle)射流中的物理过程,本文应用平面激光诱导荧光技术对一个大尺度的水射流进行了实验研究。流场显示的实验结果表明不定源喷嘴在射流的剪切层引入了蘑菇形反向旋转的涡对。这些涡的矢量方向与射流方向相同或相反,被称为流向涡(streamwise vortex)。由于射流中存在开尔文一亥姆霍兹不稳定,每当一个横向涡(spanwisevortex,即涡的矢量方向与射流方向垂直)从喷嘴脱流时会产生瞬时的低压,该瞬时低压促使向内发展的流向涡对在喷嘴的凹槽处生成。这些涡对在向下游流动的过程中会重组并在喷嘴的尖峰面生成向外发展的涡对。这些流向涡极大地影响了射流的发展。流向涡与横向涡的相互作用促使射流更早地发展成为湍流。由于流向涡同时也在射流中引入了径向的剪切流动,因此导致了更多的湍流生成从而增强了射流与周围流体的混合。  相似文献   

7.
使用大涡模拟方法对冲击面为平面的超声速中等欠膨胀冲击射流进行了数值模拟.利用三阶迎风和四阶对称紧致格式对无量纲化轴对称可压缩滤波N-S方程进行空间离散,时间上推进采用的是三阶精度的TVD型Rugge-Kutta法. 通过与经典的冲击射流实验比较,证实了程序的可靠性. 数值模拟得到了流场中不同尺度的涡结构和激波结构,观察到了上行声波和反射波以及流场中不同位置的声源,分析了冲击区剪切层附近区域的压强和涡旋转强度变化的频率、冲击平板上的压强变化频率以及射流剪切层中不同位置的涡合并出现的频率,发现冲击区剪切层附近区域的压强和涡强度变化以及射流剪切层中的涡合并现象和离散频率的冲击单音有重要关联.   相似文献   

8.
本文对有限分析解法的近似计算方法及其对计算精度的影响进行了数值计算和分析讨论;然后采用有限分析解法,对前、后壁壁缘高度不同的三种腔内流场运动发展过程及腔口剪切层运动情况作了数值计算,得到的腔口剪切层上腔口随边相互作用情况与对应腔的流场显示实验结果进行了比较,两者一致,计算结果表明,采用本文发展的近似方法计算可靠,可以较大地提高计算效率。  相似文献   

9.
台阶式溢洪道滑行水流水面线和消能效果的试验研究   总被引:4,自引:0,他引:4  
通过模型试验研究了台阶式溢洪道滑行水流的流态、水面线和消能效果。试验得出,台阶式溢洪道的水流流态分为台阶内部的旋滚流态和虚拟底板以上主流区的流态。台阶式溢洪道水面线的变化与来流量、台阶尺寸和掺气浓度有关。当水流进入台阶段时,水面由于失重有一定的降低,然后逐渐抬高至某一高度后再略有降低;在掺气发生点以前,水面线沿程降低,掺气发生点以后,水面线沿程升高;当水流掺气饱和时,水深沿程不再变化,为明渠均匀流。台阶式溢洪道的消能率是逐级台阶的累积效应。水流通过与台阶之间的碰撞、台阶上的水流漩滚以及水流内部的紊动剪切强化了溢洪道的消能效果。在试验范围内,台阶式溢洪道与光滑溢洪道比较,消能率可以提高40% ~70%。通过试验,得出了台阶式溢洪道滑行水流水面线和消能率的计算方法。  相似文献   

10.
气固两相流场的湍流颗粒浓度理论模型   总被引:8,自引:0,他引:8  
本文进行了气固两相流动颗粒湍流扩散现象的理论分析,提出了颗粒湍流扩散系数和气流弥散效应二个颗粒湍流模化新概念,在此基础上建立了气固两相流场湍流颗粒浓度模型。理论模型包括离心力和其它外加力场作用下颗粒运动和浓度分布的计算方法。运用湍流颗粒浓度模型,对直管气固两相流动、受限射流气固两相流动和90°弯管气固两相流动等三种流动做了数值模拟,计算获得颗粒速度、颗粒浓度等主要流动参数。讨论了湍流颗粒浓度模型的适用性。  相似文献   

11.
In plunging jet flows and at hydraulic jumps, large quantities of air are entrained at the intersection of the impinging flow and the receiving body of water. The air bubbles are entrained into a turbulent shear layer and strong interactions take place between the air bubble advection/diffusion process and the momentum shear region. New air-water flow experiments were conducted with two free shear layer flows: a vertical supported jet and a horizontal hydraulic jump. The inflows were partially developed boundary layers, characterized by the presence of a velocity potential core next to the entrapment point. In both cases, the distributions of air concentration exhibit a Gaussian distribution profile with an exponential longitudinal decay of the maximum air content. Interestingly, the location of the maximum air content and the half-value band width are identical for both flow situations, i.e. independent of buoyancy effects.  相似文献   

12.
The dynamic behavior of the near-field region in a coaxial variable property jet has been experimentally investigated under a swirling flow produced by rotating cylindrical inner and outer tubes, focusing on how the swirl of the outer jet affects the formation of a stagnation point in the swirling inner jet. The inner and outer jets rotate in the same direction. Air, CO2, or He is issued from the inner tube as a variable property jet, and air is issued from the outer tube in this work. In the case of a CO2 jet (a high-density, low-viscosity gas jet), a stagnation point flow is more easily formed than in the case of an air jet, and the stagnation point location is significantly lower than in that of the air jet. When the swirl of the outer jet is introduced, a stagnation point flow is more easily formed than in the case of a nonswirling outer jet, and the stagnation point location is much lower than in the case of a nonswirling outer jet. In the case of a He jet (a low-density and high-viscosity gas jet), the inner jet does not have a stagnation point flow, and its overall behavior remains nearly unchanged even under high swirl numbers of the inner and outer jets. These results clearly show that the density and viscosity differences between the inner and outer jets have a significant impact on the dynamic behavior of the near-field region in the coaxial swirling jet. The significant lowering of the stagnation point location can be physically explained by considering the theoretical equation obtained in this work.  相似文献   

13.
Viscous fingering in surfactant solutions in a rectangular Hele–Shaw cell was investigated. Test fluids were aqueous solutions of cetyltrimethylammonium bromide (CTAB) with sodium salicylate (NaSal) as a counter ion, and the ratio of mole concentration of CTAB and that of NaSal was 1–7.7. Two fluids that had a mole concentration different from that of CTAB were used. Air was injected into the cell and the growth of the interface between air and a CTAB/NaSal solution was observed. The fingertip grew similar to the finger growth in shear-thinning fluids at low pressure gradients. It took a cuspidate shape at the intermediate pressure gradient, and a sudden protrusion at a critical shear rate occurred. In high shear rate regions, the finger behaved as in a less shear-thinning fluid. These phenomena relate to rheological properties of the test fluids. Comparison with flow curves for CTAB/NaSal systems showed that the critical shear rate related to the shear rate at which a bending point appeared in the flow curve.  相似文献   

14.
The wall shear stress and the vortex dynamics in a circular impinging jet are investigated experimentally for Re = 1,260 and 2,450. The wall shear stress is obtained at different radial locations from the stagnation point using the polarographic method. The velocity field is given from the time resolved particle image velocimetry (TR‐PIV) technique in both the free jet region and near the wall in the impinging region. The distribution of the momentum thickness is also inspected from the jet exit toward the impinged wall. It is found that the wall shear stress is correlated with the large-scale vortex passing. Both the primary vortices and the secondary structures strongly affect the variation of the wall shear stress. The maximum mean wall shear stress is obtained just upstream from the secondary vortex generation where the primary structures impinge the wall. Spectral analysis and cross-correlations between the wall shear stress fluctuations show that the vortex passing influences the wall shear stress at different locations simultaneously. Analysis of cross-correlations between temporal fluctuations of the wall shear stress and the transverse vorticity brings out the role of different vortical structures on the wall shear stress distribution for the two Reynolds numbers.  相似文献   

15.
Nanoparticle dispersion and coagulation behaviors in a turbulent round jet were studied in this article. An experimental system was designed to generate a uniformly distributed air–nanoparticle two-phase flow in a turbulent round jet. The particle size distribution (PSD) was measured by a scanning mobility particle sizer (SMPS) in the near field of the jet. The particle diameters were nearly constant in the potential core due to the high carrying velocity and laminar characteristic of the flow but grew larger in the region of high turbulence intensities because the vortex structures in the mixing layer promoted coagulation. Furthermore, the migration property of small-sized nanoparticles forced them to be preserved in the potential core also leading to the diameter increase. The comparison of the particle concentration distributions at different sections indicated that the shear layer is the major region for the mixing of particle-laden stream and ambient air. The particle diameters in the axial direction experienced three stages including a slightly changed stage, an increasing stage and a constant stage. The diameter increase should be attributed to turbulence coagulation.  相似文献   

16.
An optical deflectometry system is used to provide unique space–time correlation measurements at two positions separated by varying axial distances within a high-speed jet shear layer. The measurements were made for both pure air and for helium/air mixture jets at Mach numbers M=0.9 and M=1.5. The jets issue from round nozzles and the sensing volumes at the two measurement positions consist of small light filaments along spanwise lines that are tangential to the annular jet shear layer. Applying this technique to obtain measurements detailing the level of correlation, spectral content, and convection velocity for jet flows in these flow regimes near the end of the potential core is particularly important in the understanding and prediction of jet noise. Measurements near the end of the potential core along the jet lip line exhibit distinct cross-correlation curves for the pure air jet cases. However, helium/air mixture jets display much lower levels of correlation and little evidence of large-scale structure in the measured spectra. It is believed that the thick visual density gradients dominated by smaller scales throughout the shear layer of the helium/air mixture jets effectively mask the large-scale structure, thus, reflecting a limitation of this optical deflectometer. Finally, a decrease in normalized convection velocity with helium addition is observed.  相似文献   

17.
Non-reacting experiments and numerical simulations have been performed to investigate the mixing characteristics in a supersonic combustor with gaseous fuel injection upstream of a flameholding cavity in a supersonic vitiated air flow with stream Mach number 1.7. Using helium as simulated fuel, the acetone vapor is adulterated into the fuel jet. The fuel distribution in spanwise and streamwise direction is imaged by the planar laser-induced fluorescence (PLIF) measurement. According to the similarity of experimental observations with different cavities, the typical L/D = 7 cavity with aft wall angle 45° is chosen and the flowfield with the injection is calculated by Large Eddy Simulation. Experimental and numerical results have shown that most of the fuel flow away upon the open cavity with the lifting counter-rotating vortex structures induced by the transverse jet. Only a small portion of the fuel is convected into the cavity shear layer by the vortex interaction of the jet with cavity shear layer, and then transported into the cavity due to the cavity shear layer motion and the interaction of the shear layer with the cavity trailing edge.  相似文献   

18.
为研究聚能金属射流对固体火箭发动机的冲击响应,开展了聚能装药空射实验及某尺寸发动机在无防护情况下的射流冲击实验,使用高速摄影仪记录了爆炸响应过程,并测量了不同距离及方向的空气超压和破片速度。利用AUTODYN有限元计算软件对实验过程进行了数值模拟,通过调整流固耦合的网格大小,避免了耦合泄漏。实验结果表明,火箭发动机受到射流冲击后,会发生剧烈爆炸,推进剂完全反应,破片速度达4 700 m/s以上,距离发动机爆炸中心1 m处的空气超压达到19.78 MPa,爆炸中心温度达到3 000 ℃以上,该推进剂爆炸能量略高于常规炸药。模拟结果显示,射流以头部速度7 000 m/s的速度冲击发动机壳体后,射流头部的尖端被严重烧蚀,且速度降至约5 600 m/s;推进剂在受到射流侵彻1~2 mm后,发生剧烈反应;爆炸冲击波以球形沿圆柱孔装药传播,并通过圆柱形中心孔冲击另一侧推进剂,发生装药的二次冲击起爆,同时伴有回爆现象,在推进剂中心的高斯点出现了3次超压波峰;距离发动机中心1 m处3个高斯点的平均空气压力峰值为18.75 MPa,与实验结果吻合较好。  相似文献   

19.
A hot-wire concentration probe with a spatial resolution of 0.13 mm is used to measure concentration in a model cylindrical combustor. The flow inside the combustor is simulated by injecting a helium jet into a cylindrical confinement with or without swirling air flow present. Mean concentrations are essentially zero outside of the jet region, indicating complete confinement of the scalar field by the swirling flow. Consequently, concentration fluctuations are found to be relatively weak compared to velocity fluctuations, and are maximum off-axis at a point which corresponds to the interface between helium and air flows. However, in the absence of a swirling air flow, the helium diffuses quickly to fill the combustor. The resulting helium concentrations are constant and do not resemble the jet-like behavior of the velocity field.A version of this paper was presented at the ASME Winter Annual Meeting of 1984 and printed in AMD, Vol. 66  相似文献   

20.
This paper presents a combined experimental and numerical study of the flow characteristics of round vertical liquid jets plunging into a cylindrical liquid bath. The main objective of the experimental work consists in determining the plunging jet flow patterns, entrained air bubble sizes and the influence of the jet velocity and variations of jet falling lengths on the jet penetration depth. The instability of the jet influenced by the jet velocity and falling length is also probed. On the numerical side, two different approaches were used, namely the mixture model approach and interface-tracking approach using the level-set technique with the standard two-equation turbulence model. The numerical results are contrasted with the experimental data. Good agreements were found between experiments and the two modelling approaches on the jet penetration depth and entraining flow characteristics, with interface tracking rendering better predictions. However, visible differences are observed as to the jet instability, free surface deformation and subsequent air bubble entrainment, where interface tracking is seen to be more accurate. The CFD results support the notion that the jet with the higher flow rate thus more susceptible to surface instabilities, entrains more bubbles, reflecting in turn a smaller penetration depth as a result of momentum diffusion due to bubble concentration and generated fluctuations. The liquid average velocity field and air concentration under tank water surface were compared to existing semi-analytical correlations. Noticeable differences were revealed as to the maximum velocity at the jet centreline and associated bubble concentration. The mixture model predicts a higher velocity than the level-set and the theory at the early stage of jet penetration, due to a higher concentration of air that cannot rise to the surface and remain trapped around the jet head. The location of the maximum air content and the peak value of air holdup are also predicted differently.  相似文献   

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